WO1996010716A1 - Energy converter using imploding plasma vortex heating - Google Patents
Energy converter using imploding plasma vortex heating Download PDFInfo
- Publication number
- WO1996010716A1 WO1996010716A1 PCT/US1994/011020 US9411020W WO9610716A1 WO 1996010716 A1 WO1996010716 A1 WO 1996010716A1 US 9411020 W US9411020 W US 9411020W WO 9610716 A1 WO9610716 A1 WO 9610716A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fuel
- chamber
- heating system
- air
- heat transfer
- Prior art date
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 75
- 239000000446 fuel Substances 0.000 claims abstract description 183
- 238000002485 combustion reaction Methods 0.000 claims abstract description 94
- 238000012546 transfer Methods 0.000 claims abstract description 60
- 239000000203 mixture Substances 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims description 35
- 239000006200 vaporizer Substances 0.000 claims description 18
- 239000006185 dispersion Substances 0.000 claims description 14
- 238000004891 communication Methods 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 8
- 239000003989 dielectric material Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 4
- 230000001681 protective effect Effects 0.000 claims description 3
- 239000012809 cooling fluid Substances 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims 1
- 229910045601 alloy Inorganic materials 0.000 claims 1
- 230000003134 recirculating effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 26
- 239000004020 conductor Substances 0.000 description 12
- 239000002245 particle Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000010276 construction Methods 0.000 description 5
- 230000002459 sustained effect Effects 0.000 description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 4
- 239000003574 free electron Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 230000008016 vaporization Effects 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 206010011469 Crying Diseases 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000002305 electric material Substances 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000013517 stratification Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229910000851 Alloy steel Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 101100270435 Mus musculus Arhgef12 gene Proteins 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000010891 electric arc Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- CNQCVBJFEGMYDW-UHFFFAOYSA-N lawrencium atom Chemical compound [Lr] CNQCVBJFEGMYDW-UHFFFAOYSA-N 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
- F28D7/022—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of two or more media in heat-exchange relationship being helically coiled, the coils having a cylindrical configuration
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C3/00—Combustion apparatus characterised by the shape of the combustion chamber
- F23C3/006—Combustion apparatus characterised by the shape of the combustion chamber the chamber being arranged for cyclonic combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C9/00—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C99/00—Subject-matter not provided for in other groups of this subclass
- F23C99/001—Applying electric means or magnetism to combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/02—Liquid fuel
- F23K5/08—Preparation of fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23K—FEEDING FUEL TO COMBUSTION APPARATUS
- F23K5/00—Feeding or distributing other fuel to combustion apparatus
- F23K5/02—Liquid fuel
- F23K5/14—Details thereof
- F23K5/22—Vaporising devices
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/0027—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters using fluid fuel
- F24H1/0045—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters using fluid fuel with catalytic combustion
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/22—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
- F24H1/24—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers
- F24H1/26—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water mantle surrounding the combustion chamber or chambers the water mantle forming an integral body
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C2202/00—Fluegas recirculation
- F23C2202/30—Premixing fluegas with combustion air
Definitions
- the invention relates to a method and apparatus for converting energy through combustion of fuel by means of so-called sustained imploding vortex technology in the form of a super-heated, high velocity rotating gas mass.
- the fuel is preheated to very high temperature so as to make it chemically and molecularly highly active and to enclose the preheated fuel so that it forms an insulated ionizing energy ball, containing large numbers of free electrons.
- the electrons are believed to attach themselves to the activated fuel molecules, causing the fuel to behave as an ionized plasma within a combustion chamber.
- the plasma form of the gas greatly increases the combustion efficiency which further increases the temperature of the plasma. Diesel oil that normally burns at 1200° F.
- the flow patterns within the plasma vortex are of significant impor ⁇ tance in the operation of the system in that they create and sustain an implosion within the combustion chamber and a heat collection chamber connected thereto. It is accordingly a primary object of the invention to maximize thermal combustion efficiency by means of imploding vortex technology.
- the sustained imploding vortex mentioned above is de ⁇ fined as a system of stratified gas plasma wherein the heavier particles of the gas masses become progressively stratified in parallel with the outer perimeter of the vortex and the lighter particles of the gas masses become progressively stratified around the central core of the vortex.
- Rotating vortices of gas plasma form a gravita ⁇ tional gradient causing the heavier gas particles to drift to the outer perimeter and the lighter particles to the central core. It is also demonstrable that the temperature of the center of the vortex is relatively cool when compared with the temperature at its periphery.
- the invention utilizes all of the characteristics of the imploding vortex technology to its advantage so as to increase the combustion efficiency and to greatly reduce and/or eliminate polluting emissions commonly associated with combustion of hydrocarbon and other fuels.
- the invention as disclosed can be used for heating an industrial boiler, a domestic or commercial hot water heater, or any heating system using liquid or air or other gas as a heat transfer medium.
- the system is also in a further development capable of generating electrical current by the known principles of Magneto Hydrodynamics.
- U.S. Patent No. 2,747,526 shows a cyclone furnace wherein a granular solid fuel is directed in a high velocity stream of superatmospheric pressure carrier air directed tangentially into a fluid-cooled cyclone chamber.
- U.S. Patent No. 3,597,141 discloses a burner for gaseous, liquid pulverized fuel, which has a tubular burner structure of a rotationally symmetrical shape, and which has nozzles for supplying combustion air tangentially into the combustion chamber.
- U.S. Patent No. 4,297,093 discloses a combustion method which can reduce the emission of NOx and smoke by means of a specific flow pattern of fuel and combustion air in the combustion chamber, and wherein secondary air is injected to create a swirling air flow.
- the invention is based on the principle of imploding plasma dynamics ("I.P.D.") wherein sustained implosion is maintained in the form of a super-heated, high velocity imploding vortex in a suitably shaped combustion chamber which leads to creation of plasma combustion super-heating and ionizing of the fuel within an ionizing chamber inside a vortex chamber prior to combustion.
- the system is constructed to maximize laminar flow in the vortex so as to stratify molecular and atomic articles by particle mass.
- the resulting flow pattern operates to drive the heavier particles into the very hot peripheral pressure strata where they release their kinetic energy before they return as lighter gases to the low pressure at the central core of the vortex, causing a repetition of the cycle.
- the inventive concept also includes elec ⁇ trically insulating the combustion and ionizing fuel chamber in such a way as to use these chambers as electrodes so as to supply an electric current by the prin- ciple of magneto-hydrodynamics.
- a heating system for heating a heat sink via a heat transfer medium.
- the invention includes a vortex chamber having opposite first and second inwardly curved end walls, a combustion chamber fluidly communication with the vortex chamber, fuel-air supply means fluidly communicating with the combustion chamber for injecting fuel-air mixture into the combustion chamber. Ignition means are provided in the combustion chamber for igniting the fuel-air mixture.
- a fuel ionizing chamber is disposed in the vortex chamber fluidly communicating with the fuel-air supply means for ionizing fuel entering the fuel-air supply means, and heat transfer medium containing means are provided for holding the heat transfer medium in thermal contact with the vortex chamber.
- the heating system includes an air preheat space enclosing the combustion chamber, at least one air tube having an air outlet tangentially engaging the air preheat space and an air inlet, and an air blower connected to the air inlet for injecting air into the air preheat space for generating a vortex of preheated air in the air preheat space.
- a fuel dispersion unit in the combustion chamber, fluidly communicating with the fuel ionizing chamber for dispersing fuel into the combustion chamber.
- the heating system includes in the fuel-air supply means a fuel vaporizer having a fuel inlet fluidly communicating with the fuel source, and a fuel outlet fluidly communicating with the fuel ionizing chamber, further including fuel dispersing means in the fuel ionizing chamber, a fuel baffle in the fuel dispersing means, a pedestal supporting the baffle in the fuel ionizing chamber, and at least one weeping hole in the pedestal for releasing fuel accumulating in the fuel ionizing chamber.
- the heating system includes electric insulating means for electrically insulating the fuel-ionizing chamber from the vortex chamber, and a plurality of apertures in the fuel dispersion unit for passing ionized fuel into the combustion chamber.
- An exhaust tube fluidly communicating with the vortex chamber is provided for exhausting burnt fuel air mixture, and a fuel tube disposed coaxially within the exhaust tube in- fluid communication with the fuel vaporizer.
- the electric insulating means include a first circular electric insulator in the fuel tube for electrically insulating the fuel ionizing chamber from the fuel vaporizer, a tubular connection between the fuel ionizing chamber and the fuel dispersion unit, and a one way check valve can be inserted in the tubular connection for preventing oxygen from accidentally entering the ionizing chamber from the combustion chamber and possibly causing ignition in the fuel ionizing chamber via the fuel dispersion unit.
- the invention further includes a heat sink in fluid communication with the heat transfer containing means, and wherein the heat transfer medium is a liquid or gaseous fluid, and further a plurality of heat transfer chambers in the heat transfer medium containing means, each of the heat transfer chambers containing a respective heat transfer medium in fluid communication with a respective heat sink.
- Figure 2 is a diagrammatic cross-sectional view of the invention showing a heat transfer coil
- Figure 3 is an elevational diagrammatic cross-section ⁇ al fragmentary view of the invention showing a multi-media heat transfer arrangement
- Figure 4 is an elevational diagrammatic cross-section ⁇ al view of the invention showing a version with external exhaust gas return;
- Figure 5 is an elevational diagrammatic cross-section ⁇ al view of the invention showing atmospheric air used for heat transfer medium
- Figure 6 is an elevational diagrammatic fragmentary view of the invention showing a heat exchanger component
- Figure 7 is an elevational diagrammatic cross-section ⁇ al view of the invention showing a fuel vaporizing element
- Figure 8 is an elevational diagrammatic cross-section ⁇ al view of the invention showing another fuel vaporizing element
- Figure 9 is an elevational diagrammatic cross-section ⁇ al view of the invention showing a third version of a fuel vaporizing element
- Figure 10 is an elevational diagrammatic cross-sec ⁇ tional view of the invention showing a fuel vaporizer with a reticulated heating core;
- Figure 11 is an elevational diagrammatic cross-sec- tional view of the invention seen along the line 11-11 of Fig. 10;
- Figure 12 is a plan diagrammatic cross-sectional view of the invention showing a fuel vaporizer with a porous core
- Figure 13 is a plan cross-sectional view of the invention seen along the line 13-13 of Fig. 12;
- Figure 14 is a sectional elevational view of the invention showing a heating system with ultrasonic fuel delivery transducer, seen along the line 14-14 of Fig. 14a;
- Figure 14a is a sectional top-down view of the heating system according to Fig. 14;
- Figure 14b is a diagrammatic sectional view of the ultrasonic delivery transducer of Fig. 14 and 14a, showing structural details of the transducer.
- a vortex chamber 1 has a substantially cylindrical wall 2, enclosed by first and second inwardly curved end walls 3 and 4.
- a combustion chamber 6 is fluidly communicating through second end wall 4 with the vortex chamber 1, and has an air inlet 7 receiving air from an air compressor 8 via an air inlet tube 11 and a circular air space 9 surrounding the combustion chamber 6 which serves to preheat inlet air before it enters the combustion chamber 6.
- compressor cut-off means may be provided for turning off the compressor 8, and instead opening a choke plate 30 that operates to admit air directly into the air inlet 7 of the combustion chamber 6.
- Such compressor cut-off means would advantageously include a pressure gauge at the inlet of the combustion chamber 6, actuating means responsive to the pressure gauge coupled to the choke plate 30, and compressor cut-off means also coupled to the pressure gauge for de-energizing the compressor 8.
- Fuel in gaseous or vapor form enters the combustion chamber 6 from a fuel inlet 12 in either gaseous or liquid form via a check valve 13 and, in case of liquid fuel, a vaporizer 14 with a heating coil 16 as described in more detail below.
- the fuel continues through a fuel tube 17, advantageously disposed coaxially within an exhaust tube 18 which provides an exhaust gas escape from the vortex chamber 1. In traversing the fuel tube 17 the fuel becomes even more heated by means of heat transfer from the exhaust tube 18.
- the fuel enters a fuel ionizing chamber 19 disposed substantially centrally in the vortex chamber 1 wherein the fuel is ionized as described in more detail below, and continues downward through the fuel tube extension 21 to a fuel dispersion unit 22 from which fuel enters the combustion chamber through apertures in the fuel dispersion unit 22 and mixes with the preheated air entering the air inlet 7 as described above.
- the combustion chamber walls form an inward facing constriction 23 that creates a venturi in the fuel air inlet to the combustion chamber 6.
- a high voltage electric supply is connected via conductors 26 and 26a to the fuel dispersion unit 22 creating electric arcs between the fuel dispersion unit 22 and the constriction 23 which ignite the fuel air mixture in the combustion chamber 6.
- a vortex of burning fuel-air mixture is created in the combustion chamber by means of the air being fed tangentially by the air tube 11 from compressor 8 into the cylindrical air space 9, as indicated by arrows A.
- the rotation of the vortex intensifies as the burning fuel-air mixture expands in the combustion chamber 6, and escapes upward through the upper outlet of the combustion chamber 6, forming an extended outer vortex indicated by arrow C which follows the inner wall surface of the vortex chamber 1 in an upward moving spiral motion.
- the vortex As the outer vortex C formed of still burning and expanding air-fuel mixture approaches the inward curved upper first end wall 3, the vortex is turned into an inner vortex D that axially changes direction downward while retaining its rotational direction, but at a greatly increased rotational speed due to the reduction of the diameter of the vortex. As the inner vortex reaches the lower second end wall 4 it is forced outward to merge with the outer vortex C, and thereby repeats the entire cycle of rotating gases forming a system of a so-called imploding gas plasma vortex, wherein a very high pressure and temperature condition is created in the region of the outer vortex and relatively low pressure and low temperature but very high speed is created in the region of the inner vortex.
- Electric charges are created due to the high rotational speed and resultant gravitational gradient by the plasma in the vortices formed in the vortex chamber 1, and an electric potential differential is formed between the inner structures of the vortex chamber, i.e. the ionizing chamber 19 and the fuel tube 17 and its lower extension 21.
- Electric insulator 27 is therefore inserted in the fuel tube 17 and fuel tube extension 21, and insulator 29 serves to insulate the electric conductor 26a.
- the vortex chamber 1 is advantageously provided with a heat-protective lining 34 of graphite, ceramic or other high temperature-resistant material especially at the bottom end wall 4 proximal to the outlet of the combustion chamber 6 where the temperature is especially high.
- a heat protective ring 36 also of a highly heat-resistant material.
- An expansion relief valve 25 at the top of the heat transfer medium container 31 serves to relieve excessive pressure in the container 31.
- the operation of the invention leads to a high degree of efficiency of the combustion process.
- the heat generated by the combustion in the vortex chamber is transferred through the walls 2 of the vortex chamber to a heat transfer medium, gaseous or liquid, contained in heat transfer medium container 31 for containing either liquid, e.g. water or gas e.g. air as heat transfer media which is connected via inlet 32 and outlets 33' and 33" to an external heat sink, not shown.
- the operation of the invention includes starting the air supply blower 24 so as to start the pattern of vortex rotation.
- the air enters the system tangentially at the upper and outer air space 9 in air tube 11 causing the air to move in a helical and downward spiral path forming the vortex indicated by arrow 19' at the inlet end 7 of combustion chamber 6, where it enters the venturi 23 of the combustion chamber and causes the air masses in the combustion chamber 6 to move in a substantially upward- moving helical path.
- the venturi creates a low pressure region.
- the vortex at this region increases in velocity, creating a high pressure at its periphery and a low pressure at its central core.
- the fuel next passes into the vapor dispersing unit 22.
- a high-voltage electric current is passed through conductors 26, 26a connected to the fuel dispersing unit causing an electric arc to form between the dispersing unit 22 and the sides of the venturi, causing ignition of air mixture.
- a very high temperature rise is created within the combusting chamber, in turn forming the very high velocity and high temperature imploding vortex, first in the combustion chamber and next in the vortex chamber serving as a heat collecting chamber.
- the ionizing chamber 19 becomes continuously bathed in the free electrons set free by the high velocity vortices created by the imploding combustion.
- the free electrons drift to the center so they can readily move into the ionizing fuel chamber 19 and attach themselves to the gasified fuel particles that then cause the fuel vapor to behave as a plasma.
- the center region of the implosion is at relatively low speed and cool temperatures as compared to the conditions at the outer periphery. A test performed on a working system show several hundreds of degrees F. temperature at its center, as compared to thousands of degrees at its perimeter.
- the ionizing chamber 19 is therefore located in a safe zone and keeps the fuel temperature at a desired level.
- the combustion and vortex chambers (6,1) can be electrically insulated from their bases and the outer wall 31 of the heat transfer medium container.
- the combustion and vortex chambers will act as a positive electrode, i.e. anode, and the ionizing chamber 19 will act as a negative electrode i.e. cathode. It is accordingly possible to draw an electric current between the anode and cathode according to the principles of magneto hydrodynamics electricity generation.
- the magneto-hydrodynamic action can, if desired, be enhanced by introducing water, steam or potassium salts or other agents that operate to enhance the ionization of the gas plasma into the imploding vortex.
- Figure 2 shows another version of the energy converter, having the same basic elements as described above under Fig. 1 and using the same reference numerals for corresponding elements as in Fig. 1, but having a different heat transfer arrangement, composed of a tubular coil 37 of a good heat-conducting material such as copper or aluminum, having an inlet port 38 and an outlet port 39, in thermal contact with the wall 2 of the vortex chamber 1.
- the coil 37 may, for example, be traversed by a heat trans ⁇ ferring liquid such as water or glycol and/or powdered aluminum.
- a heat trans ⁇ ferring liquid such as water or glycol and/or powdered aluminum.
- the vortex chamber may also in this case be surrounded by a heat transfer medium container 31, which can be used for transferring heat, especially to a gaseous heat transfer medium, such as air or the like, by means of suitably located respective inlets and outlets 32, 33.
- a heat transfer medium container 31 which can be used for transferring heat, especially to a gaseous heat transfer medium, such as air or the like, by means of suitably located respective inlets and outlets 32, 33.
- Such a construction is well suited for a residential heater as a source for both steam heated water and heated air.
- Fig. 3 shows still another embodiment derived from the embodiment shown in Fig. 1, but not showing the combustion chamber elements since these are similar to those of Fig. 1.
- Fig. 3 shows besides the heat transfer medium container 31 as in Figs. 1 and 2 another heat transfer container 41 enclosing the container 31.
- the inner heat transfer medium container 31 is constructed for handling a liquid heat transfer medium via respective inlet 32 and outlet 33
- the outer heat transfer medium container 41 is intended for handling gaseous heat transfer medium, e.g. air, driven by a blower 42 in a circular path through the air space 40 between the walls of containers 31 and 41 through an air inlet opening 43 and out through an air outlet opening 44, thereby attaining a very high degree of efficiency of the heat energy transfer.
- gaseous heat transfer medium e.g. air
- Fig. 4 shows an embodiment similar to that of Fig. 1, but is provided with the feature that part of the exhaust gas leaving the exhaust tube 18 is captured by a bell 47 ducted by means of a duct 48 to an input 49 of the air compressor 8, so that part of the exhaust gas is recirculated back into the combustion chamber via compressor 8 which has the advantage that the amount of unburned emissions such as carbohydrates and CO are reduced.
- the lower fuel tube extension 21 has a number of weep- ing holes 46 in the ionizing chamber 19 so that condensed liquid fuel that may accumulate there can escape via the lower fuel tube extension 21.
- Fig. 5 shows an embodiment similar to that of Fig. 1, again with the same reference numerals for the same elements, but with the outer heat transfer medium container 31 arranged to handle especially a gaseous heat transfer medium, e.g. air, being driven in a long helical path through the container 31 by a blower 42 through an air inlet 43 and out through an air outlet 44.
- a gaseous heat transfer medium e.g. air
- This embodiment is especially well suited for air heating of homes, office buildings, stores, etc., where forced air heating is often the preferred mode of heating.
- Fig. 6 shows a heat exchanger that is especially well suited for use in large building complexes such as office buildings and warehouses and the like wherein it is often impractical to distribute the heat transfer medium over larg distances by means of heated air since the air ducts required in such places require an unreasonable amount of space. In such cases it is often preferred to distribute the heat by means of a primary liquid heat transfer medium to various heat zones, each equipped with a heat exchanger for transferring heat from the liquid heat transfer medium to a secondary gaseous heat transfer medium, e.g. air, by means of a heat exchanger, of which an especially advantageous construction is shown in Fig. 6.
- a primary liquid heat transfer medium to various heat zones, each equipped with a heat exchanger for transferring heat from the liquid heat transfer medium to a secondary gaseous heat transfer medium, e.g. air, by means of a heat exchanger, of which an especially advantageous construction is shown in Fig. 6.
- hot liquid heat transfer medium e.g. water or glycol drawn from outlets 33' , 33" in Fig. 1 and 4 or outlet 33 in Fig. 2 enters as hot liquid at 47 and traverses a funnel-shaped heat transfer chamber 48 having inner walls lined with heat fins 49, cut for example as a spiral attached at one edge to the inside wall of chamber 48, and escapes from the chamber 48 via a liquid outlet 51 to return to the liquid inlet 32 of Figs. 1 and 4.
- Gaseous heat transfer medium e.g. air
- the cold air enters the bottom inlet 52, while the hot liquid enters at the top hot liquid inlet 47.
- the heat exchanger according to Fig. 6 is also very well suited for condensing steam of high temperature entering at inlet 47 to water exiting at exit 51, with cooling fluid entering at inlet 52 and exiting at exit 57
- the fuel vaporizer 14 shown in Fig. 1 serves to preheat and vaporize liquid fuel entering at fuel line 12 via a one-way valve 13.
- Various forms of fuel vaporizers are shown and described in more detail below.
- Figs. 7, 8 and 9 show various forms of fuel vaporizers 14 which can be used in all embodiments of the invention to vaporize liquid fuel.
- liquid fuel entering at fuel pipe 12 trav ⁇ erses a coiled tubular heating element 82, wherein it is vaporized and enters a vapor chamber 83,from where it exits through vapor tube 17.
- the heating element 82 is heated by current from an electric power source 86,connected thereto via conductor 87, a metallic body 88, the walls 89 of vapor chamber 83 and return path terminal 91.
- Fig. 8 shows a vaporizer of similar construction as shown in Fig. 7, but having the vapor tube 17 insulated by an electric insulator 92 from the walls 89 of the vapor chamber 83, and having an electrolyzing power source 93 connected via conductors 94, 96 to the vaporizer for applying an electrolyzing potential to the vapor tube 17, so as to electrolyze fuel vapors issuing from vapor tube 84.
- Fig. 9 shows a vaporizer having a heating element composed of series-connected concentric tubular elements 97, 98 made of resistive electric material heated by electric power source 86 via conductor 99, terminal 101, fuel pipe 12, conducting body 88 and return conductor 102.
- An outer tubular electrolyzing element 103 is connected to an electrolyzing power source 93 via conductor 103.
- the electrolyzing power source 93 is connected to electric power source 86 via conductor 104, terminal 101 and conductor 99.
- Figs. 10 and 11 show a fuel vaporizer for vaporizing large fuel flows having a liquid fuel inlet line 12 connected to fuel dispersing spray nozzle 107 which sprays fuel into a reticulated metal heating element 108 having a honey-combed cross-section as shown in Fig. 11, and which is heated by electric current supplied by an electric power source 86 via conductors 109, 111.
- the fuel is vaporized in heating element 108 and exits at fuel vapor outlet 112.
- the heating element 108 is supported within an electrically insulating containing structures indicated by reference numeral 100 so as to avoid short-circuiting the heating element.
- Figs. 12 and 13 show a vaporizer of similar construction as in Figs.
- Figs. 14 and 14a show an embodiment of the invention which is especially directed to the use of liquid fuel which enters the energy converter at arrow Al through a fuel intake pipe 201.
- the fuel intake pipe 201 communicates with a fuel nozzle 203 having an outlet 204 leading into a toroidal fuel delivery chamber 206.
- the fuel nozzle 203 is in mechanical engagement with an ultrasonic transducer 202 which imparts ultrasonic vibrations to the fuel nozzle 203.
- the transducer is connected to an ultrasonic generator 208 which energizes the transducer 202 as described in more detail below.
- the ultrasonic vibrations of the nozzle 203 operate to finely disperse the liquid fuel as it issues from the nozzle outlet 204.
- the dispersed liquid fuel issuing from the nozzle 204 enters the fuel delivery chamber 206 as a fine mist that quickly changes to a fuel vapor due to the elevated temperature of the fuel delivery chamber 206.
- the mist issuing from the nozzle will be in the form of fine droplets having a size of typically 3 to 5 microns.
- the temperature in the fuel delivery chamber 206 may typically be approximately 2000 degrees F. From the fuel delivery chamber 206 the vaporized fuel enters a fuel vapor path 209 leading to a constriction 211 of a venturi-shaped inner combustion chamber 212.
- the venturi-shaped combustion chamber 212 is formed of a cylindrical wall 213 formed of a suitable high-temperature material capable of withstanding the intense heat of the inner combustion chamber 212.
- Inlet combustion air enters the system at air inlet 200 shown at arrow A2 through an air pipe 214, which enters a cylindrical air pre-heating chamber 216 in tangential direction as seen in Fig. 14a thereby setting the combustion air in circular motion as indicated by arrows A3.
- a spark plug 218 has an electrode 219 rising inside the lower part 217 of the combustion chamber 212 to the center of the constriction 211 of the venturi chamber 212, where it ignites the fuel-air mixture.
- the air descends in circular motion through the preheating chamber 216 and rises through the combustion chamber lower part 217, the air is set in an ever faster swirling motion as it reaches the constriction 211, while it is simultaneously preheated.
- the vortex becomes a so-called imploding vortex wherein the air reaches a very high velocity as it is ignited.
- the fuel-air mixture becomes intimately integrated which insures a very high combustion efficiency.
- the burning and swirling air mass rising through the combustion chamber upper part 222 turns into a high temperature plasma vortex.
- venturi action at the center of the constriction 211 of the venturi chamber 212 creates a vacuum within the fuel chamber which maintains the temperature at the constriction at a relatively low value which protects the material forming the venturi constriction against excessive temperatures.
- the combusted gases leave the combustion chamber as indicated by arrows A4 to enter the receiving chamber, e.g. chamber 1, seen in Fig. 1.
- Fig. 14b shows an exemplary version of the transducer 202 inserted between the fuel intake pipe 201 and the nozzle 203.
- Many types of transducers are known which operate to impart ultrasonic vibrations to a liquid.
- This figure shows a transducer formed of two washer-like elements 231,232 made of piezoelectric material. The elements 231,232 are cemented together via a center electrode 233, connected to one pole 234 of the ultrasonic generator 208, while the outsides of the piezo elements have electrodes 237 connected in parallel to the other pole 236 of the ultrasonic generator 208.
- the piezo-electric material of the two piezo-elements are structured so that they respectively contract and expand in opposite directions, causing the center part of the piezo-elements to bend back and forth in axial direction along axis 238 of the transducer.
- the washer-like piezo-electric elements 231,232 are suspended along their outer perimeters in a circular elastic matrix 241 which allows the elements to vibrate in the matrix.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Spray-Type Burners (AREA)
- Investigating, Analyzing Materials By Fluorescence Or Luminescence (AREA)
- Saccharide Compounds (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Finger-Pressure Massage (AREA)
- Plasma Technology (AREA)
- Thermotherapy And Cooling Therapy Devices (AREA)
- Combustion Methods Of Internal-Combustion Engines (AREA)
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/896,610 US5359966A (en) | 1992-06-10 | 1992-06-10 | Energy converter using imploding plasma vortex heating |
PCT/US1994/011020 WO1996010716A1 (en) | 1992-06-10 | 1994-09-30 | Energy converter using imploding plasma vortex heating |
AU79605/94A AU7960594A (en) | 1992-06-10 | 1994-09-30 | Energy converter using imploding plasma vortex heating |
DE69426610T DE69426610T2 (de) | 1992-06-10 | 1994-09-30 | Energieumwandler der die heizwirkung eines implodierenden plasmawirbels ausnutzt |
EP94930510A EP0834039B1 (de) | 1992-06-10 | 1994-09-30 | Energieumwandler der die heizwirkung eines implodierenden plasmawirbels ausnutzt |
JP51168996A JP3639307B2 (ja) | 1992-06-10 | 1994-09-30 | 内破プラズマ渦加熱を用いたエネルギー変換器及び加熱システム |
AT94930510T ATE198787T1 (de) | 1992-06-10 | 1994-09-30 | Energieumwandler der die heizwirkung eines implodierenden plasmawirbels ausnutzt |
ES94930510T ES2156159T3 (es) | 1992-06-10 | 1994-09-30 | Convertidor de energia utilizando un calentamiento vorticial por implosion de plasma. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US07/896,610 US5359966A (en) | 1992-06-10 | 1992-06-10 | Energy converter using imploding plasma vortex heating |
PCT/US1994/011020 WO1996010716A1 (en) | 1992-06-10 | 1994-09-30 | Energy converter using imploding plasma vortex heating |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1996010716A1 true WO1996010716A1 (en) | 1996-04-11 |
Family
ID=26788435
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1994/011020 WO1996010716A1 (en) | 1992-06-10 | 1994-09-30 | Energy converter using imploding plasma vortex heating |
Country Status (8)
Country | Link |
---|---|
US (1) | US5359966A (de) |
EP (1) | EP0834039B1 (de) |
JP (1) | JP3639307B2 (de) |
AT (1) | ATE198787T1 (de) |
AU (1) | AU7960594A (de) |
DE (1) | DE69426610T2 (de) |
ES (1) | ES2156159T3 (de) |
WO (1) | WO1996010716A1 (de) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2278223A1 (de) * | 2004-05-19 | 2011-01-26 | Innovative Energy, Inc. | Verbrennungsverfahren und Verbrennungsvorrichtung |
US8968580B2 (en) | 2009-12-23 | 2015-03-03 | Suncor Energy Inc. | Apparatus and method for regulating flow through a pumpbox |
CN105509308A (zh) * | 2014-10-15 | 2016-04-20 | 王守国 | 等离子体锅炉 |
Families Citing this family (33)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5861600A (en) * | 1996-08-21 | 1999-01-19 | Jensen; Donald C. | Fuel plasma vortex combustion system |
US5944512A (en) * | 1998-08-10 | 1999-08-31 | Ludwig; Mark | Heating and incineration device |
US6908298B1 (en) | 2001-10-30 | 2005-06-21 | Owen W. Dykema | Air-fuel injection system for stable combustion |
US20050019714A1 (en) * | 2003-07-24 | 2005-01-27 | David Platts | Plasma catalytic fuel injector for enhanced combustion |
US7040258B2 (en) * | 2004-10-06 | 2006-05-09 | Rheem Manufacturing Company | Low NOx water heater with serpentined air entry |
KR100652889B1 (ko) | 2004-12-29 | 2006-12-01 | 업산건철(주) | 보일러용 버너 |
US8360760B2 (en) | 2005-03-09 | 2013-01-29 | Pekrul Merton W | Rotary engine vane wing apparatus and method of operation therefor |
US8523547B2 (en) | 2005-03-09 | 2013-09-03 | Merton W. Pekrul | Rotary engine expansion chamber apparatus and method of operation therefor |
US8794943B2 (en) | 2005-03-09 | 2014-08-05 | Merton W. Pekrul | Rotary engine vane conduits apparatus and method of operation therefor |
US8517705B2 (en) | 2005-03-09 | 2013-08-27 | Merton W. Pekrul | Rotary engine vane apparatus and method of operation therefor |
US8647088B2 (en) | 2005-03-09 | 2014-02-11 | Merton W. Pekrul | Rotary engine valving apparatus and method of operation therefor |
US8800286B2 (en) | 2005-03-09 | 2014-08-12 | Merton W. Pekrul | Rotary engine exhaust apparatus and method of operation therefor |
US8360759B2 (en) | 2005-03-09 | 2013-01-29 | Pekrul Merton W | Rotary engine flow conduit apparatus and method of operation therefor |
US8955491B2 (en) | 2005-03-09 | 2015-02-17 | Merton W. Pekrul | Rotary engine vane head method and apparatus |
US7694520B2 (en) | 2005-03-09 | 2010-04-13 | Fibonacci International Inc. | Plasma-vortex engine and method of operation therefor |
US7055327B1 (en) * | 2005-03-09 | 2006-06-06 | Fibonacci Anstalt | Plasma-vortex engine and method of operation therefor |
US8833338B2 (en) | 2005-03-09 | 2014-09-16 | Merton W. Pekrul | Rotary engine lip-seal apparatus and method of operation therefor |
US9057267B2 (en) | 2005-03-09 | 2015-06-16 | Merton W. Pekrul | Rotary engine swing vane apparatus and method of operation therefor |
US8689765B2 (en) | 2005-03-09 | 2014-04-08 | Merton W. Pekrul | Rotary engine vane cap apparatus and method of operation therefor |
US20120017849A1 (en) * | 2010-07-22 | 2012-01-26 | Sang Kwon Kim | Combustion apparatus with improved thermal efficiency |
US9513003B2 (en) * | 2010-08-16 | 2016-12-06 | Purpose Company Limited | Combustion apparatus, method for combustion control, board, combustion control system and water heater |
US20130074786A1 (en) * | 2011-09-26 | 2013-03-28 | Claude Lesage | Gas water heater with increased thermal efficiency and safety |
DE102014103812A1 (de) | 2014-03-20 | 2015-09-24 | Webasto SE | Verdampferbrenner für ein mobiles, mit flüssigem Brennstoff betriebenes Heizgerät |
DE102014103815B4 (de) | 2014-03-20 | 2018-07-19 | Webasto SE | Verdampferbrenner |
DE102014103817B4 (de) * | 2014-03-20 | 2018-07-19 | Webasto SE | Verdampferbrenner für ein mobiles, mit flüssigem Brennstoff betriebenes Heizgerät |
DE102014103813A1 (de) | 2014-03-20 | 2015-09-24 | Webasto SE | Verdampferbrenneranordnung für ein mobiles, mit flüssigem Brennstoff betriebenes Heizgerät |
CA2852460A1 (en) * | 2014-05-23 | 2015-11-23 | Donald J. Stein | Implosion reactor tube |
RU181270U1 (ru) * | 2017-08-10 | 2018-07-09 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Московский государственный университет имени М.В. Ломоносова" (МГУ) | Устройство температурной стратификации газа |
CA3014970A1 (en) | 2017-08-18 | 2019-02-18 | Montgomery William Childs | Electrode assembly for plasma generation |
CA3014940A1 (en) | 2017-08-18 | 2019-02-18 | Montgomery William Childs | Ion generator apparatus |
RU2672457C1 (ru) * | 2017-09-20 | 2018-11-14 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Московский государственный университет имени М.В. Ломоносова" (МГУ) | Способ температурной стратификации газа |
US11112109B1 (en) * | 2018-02-23 | 2021-09-07 | Aureon Energy Ltd. | Plasma heating apparatus, system and method |
US10871289B2 (en) * | 2018-11-27 | 2020-12-22 | Grand Mate Co., Ltd. | Smoke removal device |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2747526A (en) * | 1951-07-12 | 1956-05-29 | Babcock & Wilcox Co | Cyclone furnaces |
US3597141A (en) * | 1968-08-07 | 1971-08-03 | Siemens Ag | Burner device for fluidic fuels |
US4255116A (en) * | 1975-09-22 | 1981-03-10 | Zwick Eugene B | Prevaporizing burner and method |
US4297093A (en) * | 1978-09-06 | 1981-10-27 | Kobe Steel, Ltd. | Combustion method for reducing NOx and smoke emission |
US4364724A (en) * | 1978-06-02 | 1982-12-21 | Forenade Farbiksverken | Method and apparatus for dosing an air-fuel mixture in burners having evaporating tubes |
US4758153A (en) * | 1985-07-26 | 1988-07-19 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Vaporizer for liquid fuel for producing a fuel-air mixture |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2551183B1 (fr) * | 1983-05-20 | 1988-05-13 | Rhone Poulenc Chim Base | Procede et dispositif de combustion propre s'appliquant notamment au brulage des combustibles lourds |
US4524746A (en) * | 1984-04-09 | 1985-06-25 | Hansen Earl S | Closed circuit fuel vapor system |
US5259342A (en) * | 1991-09-11 | 1993-11-09 | Mark Iv Transportation Products Corporation | Method and apparatus for low NOX combustion of gaseous fuels |
US5333574A (en) * | 1991-09-11 | 1994-08-02 | Mark Iv Transportation Products Corporation | Compact boiler having low NOX emissions |
US5185541A (en) * | 1991-12-02 | 1993-02-09 | 21St Century Power & Light Corporation | Gas turbine for converting fuel to electrical and mechanical energy |
US5321327A (en) * | 1992-01-30 | 1994-06-14 | 21St Century Power & Light Corporation | Electric generator with plasma ball |
-
1992
- 1992-06-10 US US07/896,610 patent/US5359966A/en not_active Expired - Fee Related
-
1994
- 1994-09-30 ES ES94930510T patent/ES2156159T3/es not_active Expired - Lifetime
- 1994-09-30 WO PCT/US1994/011020 patent/WO1996010716A1/en active IP Right Grant
- 1994-09-30 DE DE69426610T patent/DE69426610T2/de not_active Expired - Fee Related
- 1994-09-30 EP EP94930510A patent/EP0834039B1/de not_active Expired - Lifetime
- 1994-09-30 AT AT94930510T patent/ATE198787T1/de not_active IP Right Cessation
- 1994-09-30 AU AU79605/94A patent/AU7960594A/en not_active Abandoned
- 1994-09-30 JP JP51168996A patent/JP3639307B2/ja not_active Expired - Fee Related
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2747526A (en) * | 1951-07-12 | 1956-05-29 | Babcock & Wilcox Co | Cyclone furnaces |
US3597141A (en) * | 1968-08-07 | 1971-08-03 | Siemens Ag | Burner device for fluidic fuels |
US4255116A (en) * | 1975-09-22 | 1981-03-10 | Zwick Eugene B | Prevaporizing burner and method |
US4364724A (en) * | 1978-06-02 | 1982-12-21 | Forenade Farbiksverken | Method and apparatus for dosing an air-fuel mixture in burners having evaporating tubes |
US4297093A (en) * | 1978-09-06 | 1981-10-27 | Kobe Steel, Ltd. | Combustion method for reducing NOx and smoke emission |
US4758153A (en) * | 1985-07-26 | 1988-07-19 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Vaporizer for liquid fuel for producing a fuel-air mixture |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2278223A1 (de) * | 2004-05-19 | 2011-01-26 | Innovative Energy, Inc. | Verbrennungsverfahren und Verbrennungsvorrichtung |
US7914280B2 (en) | 2004-05-19 | 2011-03-29 | Innovative Energy, Inc. | Combustion method and apparatus |
US8968580B2 (en) | 2009-12-23 | 2015-03-03 | Suncor Energy Inc. | Apparatus and method for regulating flow through a pumpbox |
CN105509308A (zh) * | 2014-10-15 | 2016-04-20 | 王守国 | 等离子体锅炉 |
Also Published As
Publication number | Publication date |
---|---|
EP0834039A1 (de) | 1998-04-08 |
AU7960594A (en) | 1996-04-26 |
EP0834039A4 (de) | 1999-06-09 |
ES2156159T3 (es) | 2001-06-16 |
DE69426610T2 (de) | 2001-08-09 |
EP0834039B1 (de) | 2001-01-17 |
JP3639307B2 (ja) | 2005-04-20 |
ATE198787T1 (de) | 2001-02-15 |
DE69426610D1 (de) | 2001-02-22 |
US5359966A (en) | 1994-11-01 |
JPH10509504A (ja) | 1998-09-14 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0834039B1 (de) | Energieumwandler der die heizwirkung eines implodierenden plasmawirbels ausnutzt | |
US3358731A (en) | Liquid fuel surface combustion process and apparatus | |
US5321327A (en) | Electric generator with plasma ball | |
US5968378A (en) | Fuel plasma vortex combustion system | |
KR100766739B1 (ko) | 기화 연료의 연소에 의한 동력 발생 방법 및 장치 | |
US3841824A (en) | Combustion apparatus and process | |
US2385833A (en) | Fuel vaporizer for jet propulsion units | |
CN101285590B (zh) | 电动旋流器、燃烧装置以及其使用方法 | |
US5185541A (en) | Gas turbine for converting fuel to electrical and mechanical energy | |
EP1904789B1 (de) | Katalytische brennkammer und verfahren dafür | |
US4176637A (en) | Apparatus for electrostatic fuel mixing | |
CN103925116A (zh) | 滑动弧点火装置 | |
US1273466A (en) | Fuel-burner. | |
US2539165A (en) | Dispersible fuel burner having a reverse gas flow flame stabilizer | |
US3914096A (en) | Device for vaporizing fuel oil | |
CN104235875B (zh) | 伞状点火装置 | |
US3808056A (en) | Burner means for thermoelectric generator | |
US3598090A (en) | Vapor generator | |
RU2731081C1 (ru) | Способ факельного сжигания топливовоздушной смеси и устройство для реализации способа с использованием электроионизационного воспламенителя | |
US2486481A (en) | Liquid fuel burner | |
CN101443593A (zh) | 燃烧器 | |
US3932109A (en) | Ultrasonic burner means | |
CN109307264B (zh) | 基于液态燃料的微型燃烧器 | |
KR100384645B1 (ko) | 액체연료 연소장치용 버너 | |
RU2181462C1 (ru) | Горелочное устройство |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AU BR CA CN CZ FI HU JP KR NO NZ PL RO RU SK UA |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) |
Free format text: CN,CZ |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1994930510 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 1994930510 Country of ref document: EP |
|
WWG | Wipo information: grant in national office |
Ref document number: 1994930510 Country of ref document: EP |